LIVING POLYMERIZATION OF OLEFINS TO PRODUCE COPOLYMER

Abstract: The present invention provides a process for the living polymerization of aromatic, preferably styrenic monomers initiated from a living polyolefin, particularly polyisobutylene, chain end and thereby provides an efficient method for the preparation of block copolymers having polyolefin mid-blocks and styrenic end blocks. Polyisobutylene mid-blocks and styrenic end blocks comprising para-methylstyrene alpha-methylstyrene, indene and the like are preferred.

Description: Title: LIVING POLYMERIZATION OF OLEFINS TO PRODUCE COPOLYMER This application is a continuation-in-part of copending U.S. Serial Application No. 08/137,659, filed October 15, 1993. Summary of the Invention The present invention provides a process for the living polymerization of olefins, preferably styrenic monomers, initiated from a living polyisoolefin chain end, preferably a polyisobutylene chain end. This provides, among other things, an efficient method for the preparation of copolymers and block copolymers based on polyisoolefins and styrenic monomers. Preferred monomers include isobutylene, para-methyl styrene, alpha-methylstyrene, indene and the like. Background of the Invention The living polymerization of olefins is a method utilized to control molecular weight and final product properties in polymers. The polymerizations are called living because the initiators grow only one chain per initiator molecule and the polymerization continues until monomer is exhausted rather than terminating when the chain reaches a certain length or the catalyst is exhausted. Para-methylstyrene (pMeSt) has reportedly been polymerized in a living fashion by the organic esters/BCl β initiating system (R. Faust and J.P. Kennedy; Polymer Bulletin, 19, 29 (1988)). Living polymerization of para-methylstyrene is also claimed with a 2, 4, 4-trimethylpentylchloride/titanium tetrachloride (TMPCl/TiCl 4 ) initiating system in the presence of triethylamine (Et 3 N) although initiation is reportedly slow. Likewise, living polymerization has also been reportedly used to synthesize block copolymers. Y. Tsunogae and J.P. Kennedy reported the synthesis of para-methylstyrene—polyisobutylene—para- methylstyrene triblock copolymer with dicumylchloride / titanium tetrachloride / triethylamine / (DiCu Cl/TiCl4/Et3N) in 40 parts by volume methylene chloride and 60 parts by volume n-hexane (MeCl/n- hexane) at -80°C system (Y. Tsunogae and J.P. Kennedy; Polymer Bulletin, 27, 631(1992)). The triblocks manifested low tensile strength (14.1 mPa) indicating low blocking efficiency. Recently it has been discovered that living homopolymerization of isobutylene or styrene and sequential block copolymerization of said monomers can be achieved by an organic ester, ether or chloride/TiCl4 or BCI 3 initiating systems in the presence of a proton trap di-tert-butyl pyridine (DTBP) leading to block copolymers with high efficiency (R. Faust, M. Gyor, H.C. Wang, "Living Carbocationic Process", U.S. Patent Application 07/730,363 filed July 15, 1991) . The above procedure has produced low blocking efficiency with para-methylstyrene. Thus there is a need to provide a method for producing block copolymers having high blocking efficiencies. This invention meets this need. Brief Description of the Invention The present invention provides a process to produce block copolymers and new block copolymers therefrom. In general, the process comprises the living polymerization of styrenic monomers initiated from a living polymer chain end. Block copolymers having blocks of styrenic monomers and blocks of other polymers are produced. This invention also relates to a method for producing an initiator/functionalized polymer effective for polymerizing styrenic monomers by capping or functionalizing an olefin polymer with a capping compound comprising non-polymerizable monomer, preferably selected from the group consisting of: substituted or unsubstituted diphenyl alkylene, substituted or unsubstituted α-methoxystyrene, substituted or unsubstituted trans-stilbene, substituted or unsubstituted 1-isopropenyl-napthalene, and substituted or unsubstituted 2,4-dimethyl-α- methylstyrene. This capping procedure is disclosed in concurrently filed USSN 08/137,684. Description of the Preferred Embodiments This invention relates in part to the discovery that capping a living polyolefin cation with a nor_- polymerizable olefin and thereafter reacting the capped polymer with cationically polymerizable monomer is a new and efficient method to -produce block copolymers. Preferred living polyolefin cations are preferably polyisoolefin cations, even more preferably a living polyisobutylene cations (PIB+) . Preferred non- polymerizable olefins that are contacted with the living polyolefin cation are substituted or unsubstituted diphenyl alkylenes, substituted or unsubstituted α-methoxystyrenes, substituted or unsubstituted trans-stilbenes, substituted or unsubstituted 1-isopropenyl- naptha1enes, and substituted or unsubstituted 2,4-dimethyl-α- methylstyrenes. Mono or multi substitution on the aromatic ring may include methyl-, methoxy-, dimethyl-, a ino-, trimethylsiloxy-, groups and the like at different ring positions. Preferred diphenyl alkylenes include substituted or unsubstituted diphenyl ethylenes, even more preferably unsubstituted or substituted 1,1- diphenylethylenes. Hereinafter, the use of the phrase diphenyl alkylene is merely exemplary and it will be recognized by those of skill in the art that the additional capping compounds listed above may be used in a similar manner. Interestingly enough these compounds do not polymerize due to steric hindrance. For the purposes of this invention a non-polymerizable monomer is a monomer for which the thermodynamics of polymerization are so unfavorable that no polymerization to high polymer occurs. For further information concerning non-polymerizable monomers see R. Quirk, J. Ren, Makromolecular Chemie, Macromolecular Symposium, 70-71, 133, 1993, which is incorporated by reference herein. When the non-polymerizable olefin is contacted with the living polyolefin cation, a more stable carbocation is produced. This carbocation is then contacted with one or more cationically polymerizable monomers to form block copolymer. Preferred monomers include isoolefins, preferably isobutylene and styrenic monomers, preferably an alkyl styrene, more preferably para-alkylstyrene (wherein the alkyl has from 1 to 40 carbon atoms) , even more preferably para-methylstyrene. In an alternate embodiment, after capping (contacting the nonpolymerizable olefin with the living polyolefin cation) the polyolefin to produce a carbocation, when working with very reactive monomers, the Lewis acidity is decreased to a desired level by adding different amounts of metal alkoxides, preferably titanium alkoxides such as Ti[OCH(CH 3 ) 2 ]4, Ti[0(CH2) 3 CH 3 ]4 or similar organotitanium compounds. The desired level depends on the reactivity of the monomer. By decreasing the Lewis acidity, side reactions are minimized, and the polymerization is better controlled leading to high blocking efficiency. In a preferred embodiment the living polyolefin cation is any polyolefin with a terminal cationic group. Typically these polyolefins are those that are made by living polymerization methods known to those of ordinary skill in the art. These living polymers make good candidates for creating living carbocationic sites on the polymer chain specifically because of their living characteristic of being able to polymerize additional monomer, i.e. react, whenever monomer is present after the initial "polymerization" is complete. For example, polymeric carbocation can be made by reacting a living polymer with monomers that do not homopolymerize for thermodynamic reasons to form a carbocation. Such a procedure is disclosed and claimed in concurrently filed copending application USSN 08/137,684 entitled "CAPPING OF LIVING POLYMERS," herein incorporated by refe nee. In the copending application, polyolefin, p..._erably, polyisoolefin, polymultiolefin and poly( substituted or unsubstituted vinylidene aromatic compounds) more preferably polyisobutylene, is reacted with a substituted or unsubstituted compound such as diphenyl alkene (the alkene may contain from 1 to 40 carbon atoms) to create a polymer with a "cap" of the diphenyl alkene comprising a carbocation. Other compounds that can be used in place of the 1,1-diphenyl alkene are: substituted or unsubstituted diphenyl alkylenes; substituted or unsubstituted α-methoxystyrenes; substituted or unsubstituted trans-stilbenes; substituted or unsubstituted 1-isopropenyl-napthalenes; and substituted or unsubstituted 2,4-dimethyl-α- methylstyrenes. In the present invention, these "capped" polyolefins with the carbocationic site are then contacted with a cationically polymerizable monomer such as any styrenic monomer to form a "second" polymer block attached to the first polyolefin. By this method diblock, multiblock, and star copolymers can be synthesized. Multiblock copolymers, such as diblocks, triblocks and star block copolymers can be produced by careful selection of the initiator in combination with sequential monomer addition. For example, an initiator having two initiator sites can be used to produce a triblock copolymer having a polyisobutylene midblock and styrene endblocks. In a preferred embodiment one would produce a block copolymer according to this invention by polymerizing the isobutylene, capping the chain ends of the chains growing off the initiator, then adding styrenic monomer to form the end blocks. Similar methods can be used to build star polymers by choosing the appropriate initiator. A more complete discussion of the various possible initiators for diblock, triblock and star block polymers is present in U.S. Patent 4,946,899 (column 3, line 65 to column 4, line 56) , which is incorporated by reference herein. Preferred polyolefins to be capped include C4 to Ci 8 polyiso onoolefins, C4 to C1 4 polymultiolefins, and poly (substituted or unsubstituted) vinylene, vinyl or vinylidene aromatic compounds) , preferably C 4 to C^ Q polyisomonoolefins, even more preferably C4 to C 3 polyisomonoolefins. Polyisobutylene is an example of preferred isoolefin polymer. One set of reaction conditions that will produce these carbocations is, in a diluent , contact the olefin monomer with an initiating system comprising an initiator (usually an organic ether, organic ester, or organic halide) ; a co-initiator of Lewis acid (TiCl4 is a preferred co-initiator) ; and a proton trap. Preferred proton traps include substituted or unsubstituted 2,6-di-tert-butylpyridines. The co- initiator is typically used in concentrations equal to or preferably 2 to 40 times higher than the concentration of the initiator. The concentration of proton trap is preferably slightly higher than the concentration of protic impurities in the polymerization system. Any hydrocarbons and halogenated versions thereof may be used as the diluent. Methyl chloride mixed with hexane is a preferred diluent composition. The polymerization is typically conducted in a temperature range of from about -10 to about -100°C, preferably from about -50 to about -90°C for about 10 to about 120 minutes depending on the concentration of the initiator and the co-initiator. Once the desired living polymer is obtained, one or more substituted or unsubstituted diphenylethylenes are added to the polymerization media in concentrations equal up to about 10 times the concentration of the living chain ends, preferably about 1 to about 5 times the concentration of the living chain ends, even more preferably about 1 to about 2 times the concentration of the living chain ends. The di-phenylethylene is allowed to react with the living polymer for about 10 minutes to about 5 hours, depending on the concentration of the concentration of the living chain ends and the diphenylethylene. A preferred method for obtaining 100% capping of the chain ends is simply to wait. The time to wait will vary with the initiator, diphenylethylene and Lewis acid concentrations. With higher initiator concentrations the time is shorter, about 20 minutes, while lower initiator concentrations may require 10 hours to achieve 100% capping. The "capped" polyolefin, i.e. containing a carbocation, may then be contacted with one or more styrenic monomers under polymerization conditions to produce block copolymers. The polymerization may take place in any suitable reaction vessel including but not limited to glassware, autoclave reactors, tubular reactors, continuous stirred tank reactors, and other reactors known in the art. The polymerization may be run for less than a minute to over 5 hours, however longer polymerization times may be utilized depending on the final product desired. Polymerization times to reach near 100% conversion of the monomer to polymer depend on the initiator. However, for a typical commercial system polymerization times of less than 30 minutes are preferred. The reactions may also take place in solution phase, bulk phase and/or high pressure. In another embodiment the polymerization processes of this invention, both polymerizing monomer to make living polymer and using the capped living polymer as a initiator for the polymerization of styrenic monomer, may be conducted in a polymerization zone of a conventional polymerization apparatus, in the presence or in the absence of a diluent. Suitable polymerization conditions include a temperature ranging from about minus 100°C to about plus 10 β C, preferably from about minus 80°C to about 0 β C for a time period ranging from about 1 to about 180 minutes (hours) . Preferably, the polymerization reaction mixture may be subjected to agitation using conventional mixing means. The particular blocks of the block co-polymers produced by the process of the present invention may be homopolymers, copolymers, terpolymers, and the like depending upon the olefinic chargestock used. The number average molecular weight (Mn) of the block co-polymers of the present invention may range from about 500 to about 2,000,000, preferably from about 20,000 to about 300,000. The polymers have a narrow molecular weight distribution such that the ratio of weight average molecular weight to number average molecular weight (Mw/Mn) of the polymers ranges from about 1.0 to about 1.5, preferably from about 1.0 to about 1.2. The polymers may be recovered from the polymerization zone effluent and finished by conventional methods. The process of the present invention may be conducted in the presence or in the absence of a diluent. Suitable diluents include C^ to Cg halogenated hydrocarbons, such as methyl chloride, butyl chloride and methylene dichloride, C5 to C Q aliphatic hydrocarbons, such as pentane, hexane, and heptane and C5 to CIQ cyclic hydrocarbons, such as cyclohexane and methyl cyclohexane, and mixtures thereof. If solution phase is chosen, suitable diluents may be single or multi-component diluent systems that dissolve both polyisobutylene and the styrenic polymer, typical diluent or solvent mixtures usually consist of a polar solvent like methyl chloride or methylene chloride and a nonpolar solvent hexane, cyclohexane or ethylcyclohexane and the like. Polymerization temperatures may be from about -10°C to about -100°C, preferably -50°C to -90°C. Preferred monomers include cationically polymerizable monomer, preferably any aromatic monomer, including any styrenic, napthalynic or indeneyl monomer or derivatives or mixtures thereof. Preferred indenyl monomers include substituted or unsubstituted indene. Preferred napthylenic monomers include acenapthylene and the like. Preferred styrenic monomers include alkyl styrenes, preferably alkyl styrenes where the alkyl has 1 to 40 carbon atoms, preferably 1 to 10 carbon atoms. Another preferred species of monomer is ring substituted alkyl styrene, such as, para- alkylstyrene, wherein the alkyl has from 1 to 40 carbon atoms, preferably 1 to 10 carbon atoms. Specific examples of preferred monomers include alpha- methylstyrene, para-methylstyrene, indene, p-tert- butyl-styrene; p-methoxy styrene; 2,4,6, trimethyl styrene, and the like. In another embodiment the styrenic monomer may be combined with an olefin, such as isobutylene, butene, hexene, and the like, or any of the above listed monomers form a "co-polymer" block. In preferred embodiments, the styrenic monomer is combined with the polyolefin carbocation at any mole ratio depending on the final product desired. For preferred elastomeric embodiments the styrenic monomer may be present at about 20 to about 50 weight %, while for thermoplastic applications the styrenic monomer is present at up to 15 weight %, for impact modified applications the styrenic monomer may be present at 75 to 99 weight %. The product polymers are preferably diblock and triblock copolymers. Triblock copolymers preferably contain end block(s) of styrenic polymer and mid block(s) of polyisoolefin. A particularly preferred embodiment is a triblock copolymer having a polyisobutylene mid-block and para-methylstyrene end- blocks. Likewise other polyolefin-styrenic co-polymer block combinations will occur to those of ordinary skill in the art having the benefit of this disclosure. Polyisobutylene-polystyrene diblock copolymers polyisopentane-polyalpha-methylstyrene diblock copolymers, polyethylene-polystyrene diblock copolymers. Ethylene/propylene copolymer-polystyrene diblock copolymers and similar triblocks just a few of the many possible variations. A preferred aspect of this invention is that the individual block sections of the copolymers have narrow molecular weight distribution. Thus, in preferred embodiments, the molecular weight distribution can be controlled to produce a narrow unimodal distribution in each polymer block as well as the whole polymer. The combination of narrow molecular weight PIB with narrow molecular weight para-methylstyrene produces an unusually strong and unusually flexible thermoplastic elastomer with higher end use temperatures and blocking efficiency. In preferred embodiments, the block copolymers have a tensile strength greater than 15 MPa, preferably greater than 20 MPa, even more preferably, greater than 28 MPa. The block copolymers can be used in any application that thermoplastic elastomers are currently used in. For example the block copolymers can be used in molded articles, blown films, spunbondeds, nonwovens and the like. EXAMPLES In the examples that follow, molecular weight was measured by GPC method, using polyisobutylene standards. Blocking efficiency was predicted by measuring initiator efficiency. The proton trap was 2,6-di-tert-butyl-pryridine (DTBP) . Our strategy for the synthesis of PpMeSt-PIB- PpMeSt triblock was to cap the PIB chain end with 1,1- diphenylethylene (DPE) , i.e., CH 3 CH 3 PIB CH 2 C I CH 2 C I + H 2 C = C(Ph) 2 *- CH 3 CH 3 CH 3 CH 3 I I PIB CH-2 C CH 2 C CH 2 C(Ph) 2 CH 3 CH 3 and initiate pMeSt from the stable diphenyl alkyl cation. Since the diphenyl alkyl cation is more stable than the p-methylstyryl cation the Lewis acidity can now be decreased to a desired level to control the rate of homopolymerization without decreasing the crossover rate. (crossover is the initiation from or first monomer addition to the living PIB chain end, literally crossing over from isobutylene to para-methylstyrene, hence the term "crossover." POLYMERIZATION EXPERIMENTS MODELED WITH PMeSt In experiments 1, 2, 3, 4 and 5, the blocking step was modeled using 2,4,4-trimethylpentyl chloride (TPMC1) . An initiator efficiency that can be easily measured was used to predict blocking efficiency. Example 1 2,4,4-trimethylpentyl chloride, ([TMPC1]=0.002M) , was reacted with 10% more DPE (1,1-diphenylethylene) than the stoichiometric amount at the polymerization conditions i.e., TiCl 4 ([TiCl ]=0.0364 M)/methyl chloride:methylcyclohexane(MeCl:MeCH) at 40v:60v - 80°C, followed by the addition of para-methyl styrene (pMeSt) . Close to 100% initiator efficiencies were obtained at high conversions (Data are reported in Table 1) . TABLE 1 Polymerization Conversion I eff Time, min) Cil 0.5 63 54 1 70 77 2 74 87 4 82 106 8 86 109 16 100 125 EXAMPLE 2 In these modeling experiments different amounts of Ti[OCH(CH3)2]4 were added before the addition of pMeSt, but after the DPE reaction. In these experiments close to 100% initiating efficiencies are obtained even at low conversions. (Data are reported in Table 2) . TABLE 2 TiCl 4 / Time Conv • - ■■■ eff Ti [OCH ( CH 3 ) 2 ] 4 (min) (%) 2.5 78 105 7/1 4 83 118 32 100 130 8 11 137 3/1 16 16 117 66 19 123 2 3 118 3/2 8 5 118 16 6 100 EXAMPLE 3 In this example Ti[0(CH 2 ) 3 CH 3 ] 4 was used instead of Ti[OCH(CH 3 ) 2 ]4. Like Example 2, close to 100% initiator efficiencies were obtained. (Data are reported in Table 3) . TABLE 3 TiCl 4 / Polym. Conv. I eff Ti[0(CH 2 )3CH 3 ]4 Time(min) (%) (%) 1 62 92 13/3 4 78 114 32 100 134 In the following examples, hexanes were used instead of methylcyclohexane as hexanes are much less expensive. EXAMPLE 4 In these experiments TMPC1 was reacted with 3% more DPE than the stoichiometric amount at the polymerization conditions i.e., TiCl4/MeCl:HX 40v:60v, -80°C, followed by the addition of pMeSt. Lower than 100% initiator efficiencies were obtained even at high conversions indicating slow crossover reaction. EXAMPLE 5 In these experiments different amounts of Ti[OCH(CH 3 ) 2 ]4 or Ti[0(CH 2 ) 3 CH 3 ] 4 were added before the addition of pMeSt. Close to 100% initiating efficiencies were obtained. (Data are reported in Table 4) TABLE 4 TiCl 4 / Polym. Conv. I eff Ti [OCH (CH 3 ) 2 ] 4 Time (min) (%) (%) 10 30 132 3/1 40 48 119 320 70 102 10 98 102 25/7 20 100 104 τici 4 / TirθfCH- 5 ) 3 CH 3 l 1 5 98 93 3/1 21 99 100 EXAMPLE 6 PIB-PpMeSt diblock copolymers were prepared in this example using DPE and Ti(IpO)4 and were compared with results obtained in the absence of DPE and Ti(IpO)4. N-hexane/methyl chloride (HX/MeCl) mixtures were used in 60/40 v/v ratio at -80 β C. ^e [TiCl4] : [Ti(IpO)4] ratio was 25:7. 2,6-dι* tert- butylpyrine (DTBP) was used as proton trap. Concentrations during the IB polymerization were: [TiCl 4 ]=0.0364M, [DTBP]=0.004M, [TMPC1]=0.002M, [IB]o=0.354M polymerization time 20 min, V total=25 ml, [DPE]=1.03[TMPC1] (added in 1.5 ml solvent), reaction time 30 min. Ti(IpO)4 was added in 2.48 ml MeCH [TiCl4] : [Ti(IpO)4]=25:7, reaction time 10 min. 4.237 xlO-3 mol pMeSt was used; its volume with the solvent mixture was 2.15 ml. Control polymerization without DPE capping: first IB was polymerized using TMPC1 initiator followed by the addition of the pMeSt solution. Experiments with DPE capping: first IB was polymerized using TMPC1 followed by the addition of DPE, Ti(IpO)4 and the pMeSt solution. The GPC traces of the product of the control experiments (without DPE capping) are bimodal indicating large amount of unreacted PIB (estimated blocking efficiency of approximately 60%) . In contrast the GPC traces of the products obtained by our novel strategy with DPE capping and by the use of Ti(IpO) 4 demonstrate complete blocking. Similar results have been obtained with the methylcyclohexane/methyl chloride (MeCH/MeCl) 60/40, v/v solvent mixture. Example 7 The preparation of PpMeSt-PIB-PpMeSt linear and triarm-star triblock copolymers Tert-butyl-dicumylchloride (t-BudiCUCl) and tricumylchloride (TriCUCl) were used as initiators. The concentration of the functional groups was 0.002M with both initiators. MeCl/HX:40/60:v/v solvent mixture and -80°C were used. IB (isobutylene) was added in three increments. During its polymerization the concentration of the TiCl4 was 0.036M. At the end of the IB polymerization, DPE (diphenyl ethylene) was added and reacted for approximately one hour. It was followed by the addition of more TiCl4 and the introduction of Ti(IpO)4 to reach a 3:1 ratio. The system was diluted with MeCl and HX before the pMeSt addition when high molecular weight and increased viscosity were anticipated. The pMeSt was added in MeCl/HX: 40/60 solution (1 ml of pMeST solution contained 0.001906 mol of pMeSt) in one or several increments. The proton trap (DTBP) concentration was 0.004M. To maintain the DTBP concentration the pMeSt solution also contained DTBP. Other conditions are reported in table 7. In each line the top number is the amount or concentration of the reactants at -80 °C and the bottom line is the reaction time in minutes. [TiCl4] was 0.0364M during the PIB preparation and during the reaction of DPE and it was as indicated in the table during the pMeSt polymerization. TABLE 7 NO. IB(ml) DPE % [TlCl 4 ] P sol(ml) t(min} t(min) ( K ) t(min) 043093-1 17.4+17.4+5 3.87 0.0556 84.5 15+10+65 68 128 043093-2 17.4+17.4+5 17.8 0.0563 84.5 15+10+60 67 128 050793-1 17.4+17.4+5 29.4 0.0567 84.5 15+10+68 68 305 050793-2 17.4+17.4+5 32.9 0.0573 84.5 15+12+68 65 305 051493-1 17.4+17.4+5 197 0.0368 169 15+10+65 60 1100 051493-2 17.4+17.4+5 99.2 0.0367 169 15+15+60 60 1100 051893-1 17.4+17.4+5 99.5 0.0521 105 15+10+60 83 408 051893-2 17.4+17.4+5 200 0.0521 105 15+10+60 79 409 052193-1 17.4+17.4+5 100 0.0465- 5x28+29 15+10+60 65 0.0382 5x20+749 052193-2 17.4+17.4+5 100 0.0618- 5x28+29 15+10+60 77 0.0512 5x20+780 052593-1 17.4+17.4+5 104 0.0818- 5X27+18 15+10+80 65 0.0633 4X34+781 052593-2 17.4+17.4+5 98.9 0.121- 5x26+16 15+10+70 65 0.0928 4x34+750 052893-1 11.2+11.2+3.2 97.8 0.0989- 7X15 15+10+80 65 0.0832 6X20+905 052893-2 11.2+11.2+3.2 49.2 0.0969- 7x15 15+11+80 65 0.0817 6x20+905 P sol (ml) = milliliters of pMeSt solution. The stress strain properties of the above polymers are reported in tables 8a and 8b. Modulus, tensile strength and elongation at break were measured according to ASTM D 412. TABLE 8A Sample 100% 200% 300% 400% Modulus Modulus Modulus Modulus (psi/MPa) (psi/MPa) (psi/MPa) (psi/MPa) 043093-1 370/2.6 574/4.0 - - 043093-2 246/1.7 522/3.6 938/6.5 - 050793-1 452/3.1 699/4.8 1087/7.5 1549/10.7 050793-2 204/1.4 293/2.0 476/3.3 794/5.2 051493-1 371/2.6 636/4.4 1121/7.7 1746/12.0 051493-2 2168/14.9 2182/15.0 - - 051893-1 700/4.8 1071/7.4 1616/11.1 - 051893-2 912/6.3 1311/9.0 1884/13.0 2453/17.0 052193-1 753/5.2 1203/8.3 1858/12.8 2525/17.4 052193-2 1231/8.5 1592/11.0 2220/15.3 2885/19.9 052893-1 1706/11.8 1836/12.7 2243/15.5 - 052893-2 1794/12.4 1908/13.2 2438/16.8 - 052593-1 1771/12.2 2022/13.9 2551/17.6 - 052593-2 1659/11.4 2082/14.4 2668/18.4 3212/22.1 TABLE 8B Sample 500% Tensile Elongation Modulus Strength at Break (psi/MPa) (psi/MPa) (%) 043093-1 - 648.3/4.5 221.2 043093-2 - 1557/10.7 438 050793-1 - 1752/12.1 452 050793-2 1267/8.7 2171/15.0 654.3 051493-1 - 2323/16.0 473 051493-2 - 2626/18.1 285 051893-1 - 2074/14.3 384.1 051893-2 - 2792/19.3 470 052193-1 - 3043/21.0 482 052193-2 - 3123/21.5 437 052893-1 - 2495/17.2 339 052893-2 - 2348/16.2 252 052593-1 - 2902/20.0 365 052593-2 - 3238/22.3 400 Following the reaction of the DPE, 1.0 or 2.0 ml samples were taken from the reaction flask to estimate the conversion of IB to PIB and to measure the molecular weight of the PIB middle segment. The conversion of IB was generally about 100%. The PIB molecular weights and molecular weight distributions (MWD's) were calculated using PIB calibration. The triblock molecular weights and MWD's were obtained using a Gel Permeation Chromotography on line Multiangle LASER Light Scattering Detector. The Molecular weights, MWD's and the pMeSt conversions are in Table 9. The compositions of the triblocks, reported in Table 10, were calculated from the conversion and from proton NMR measurements. When the DPE was used in small excess, the MWD curves showed a broadening on the high molecular weight side, With large excesses the MWD was narrower. TABLE 9 PIB Triblock conv. No. Mn/1000 Mw/Mn Mn/1000 Mw/Mn PMeSt 043093-1 101.6 1.09 185, .2 1.69 100 043093-2 101.5 1.08 187, .4 1.86 100 050793-1 101.7 1.13 191, .7 1.13 95.1 050793-2 105.1 1.11 165, .1 1.08 61.3 051493-1 127.3 1.09 239, .1 1.08 40.6 051493-2 126.3 1.09 336, .6 1.20 100 051893-1 99.2 1.10 190, .1 1.12 85.0 051893-2 100.3 1.10 211, .6 1.23 100 052193-1 126.9 1.10 257, .0 1.12 55.4 052193-2 127.3 1.07 293, .7 1.11 70.3 052593-1 100.0 1.09 237. .1 1.23 100 052593-2 101.1 1.07 233. .5 1.26 100 052893-1 128.3 1.07 336, .9 1.36 100 052893-2 126.5 1.08 352, .9 1.44 100 TABLE 10 No. pMeSt content (NMR) pMeSt content (Calc) mol% Wt.% mol% Wt.% 043093-1 30. .8 48.4 24.0 40.0 043093-2 25. .2 41.5 24.2 40.2 050793-1 23. .2 38.8 22.9 38.5 050793-2 17. .3 30.6 16.1 28.8 051493-1 23. .4 39.1 20.5 35.1 051493-2 41. .6 60.0 38.9 57.3 051893-1 30. .9 48.5 25.0 41.2 051893-2 30. .8 48.4 28.1 45.1 052193-1 26. .7 43.5 25.7 42.1 052193-2 33. .5 51.5 30.5 48.1 052593-1 36. .3 54.6 36.1 54.4 052593-2 35. .3 53.5 35.4 53.5 052893-1 39. .1 57.5 37.7 56.1 052893-2 40. .3 58.8 37.7 56.1 TABLE 11 No. Size of the PpMeSt segments 043093-1 2 X 41,800 043093-2 2 X 42,900 050793-1 2 X 45,000 050793-2 2 X 30,000 051493-1 3 X 37,300 051493-2 3 X 70,100 051893-1 2 X 45,500 051893-2 2 X 55,700 052193-1 3 X 44,000 052193-2 3 X 55,500 052593-1 2 X 68,600 052593-2 2 X 66,200 052893-1 3 X 69,500 052893-2 3 X 75.500

Claims: Claims We claim: 1. A method of producing block copolymers comprising contacting cationically polymerizable monomer with an initiator to produce a living polymer, and thereafter contacting under polymerization conditions said living polymer with a capping compound selected from the group consisting of: substituted or unsubstituted diphenyl alkylene, substituted or unsubstituted α-methoxystyrene, substituted or unsubstituted trans-stilbene, substituted or unsubstituted 1-isopropenyl- napthalene, and substituted or unsubstituted 2,4-dimethyl-α- methylstyrene; to produce a capped polymer and contacting under polymerization conditions one or more cationically polymerizable monomers with the capped polymer. 2. A method to produce block copolymer comprising contacting cationically polymerizable monomer with a polymer capped with a compound selected from the group consisting of: substituted or unsubstituted diphenyl alkylene, substituted or unsubstituted α-methoxystyrene, substituted or unsubstituted trans-stilbene, substituted or unsubstituted 1-isopropenyl- napthalene, and substituted or unsubstituted 2,4-dimethyl-α- methylstyrene. 3. The method of claim 1 or 2 wherein the cationically polymerizable monomer is an aromatic monomer and the polymer of the capped polymer is polyisoolefin. 4. The method of claim 1 or 3 wherein the living polymer is contacted with unsubstituted or substituted diphenyl alkylene. 5. A block copolymer comprising mid-blocks of isoolefin polymer and endblocks of polymers of aromatic monomers. 6. The block copolymer of claim 5 having a narrow molecular weight distribution. 7. The block copolymer of claim 5 or 6, wherein the mid-blocks are polyisobutylene and the endblocks are polymers of styrenic monomers. 8. The use of a block copolymer produced by any of claims 1-4 as a thermoplastic elastomer. 9. The use of the block copolymer of claims 5, 6 or 7 as a thermoplastic elastomer.

Inventors: FAUST RUDOLPH, FODOR ZSOLT, FAUST, RUDOLPH, FODOR, ZSOLT
Applicants: UNIV MASSACHUSETTS AT LOWELL, UNIVERSITY OF MASSACHUSETTS AT LOWELL
Application year: 1994
Main classification: C08F297
IPC codes: C08F297